BACKGROUND
[0001] The present disclosure generally relates to flow control in fluid systems, and more
particularly to flow control in fluid systems having distributed fluid storage vessels.
[0002] Fuel systems are commonly employed to provide fuel to devices requiring chemical
energy, such as engines. The flow of fuel is typically regulated by flow control devices
like valves and throttles to match the flow of fuel to the desired output of the engine.
In some fuel systems it can be necessary to control the flow of fuel such that a breach
of the fuel system limits spillage of fuel from the fuel system. For example, fuel
tanks are commonly surrounded by an impermeable material within a berm. The berm contains
fuel in the event of leakage and the impermeable material prevents infiltration of
leaked fuel into the soil surrounding the tank. Mobile fuel tanks, such as in vehicles
may include leak detectors and typically undergo cyclic inspections to monitor for
fuel leakage.
[0003] Such systems and methods have generally been satisfactory for their intended purpose.
However, there remains a need for improved distributed fuel modules, power modules,
and methods to control fuel flow in distributed fuel modules. The present disclosure
provides a solution to this need.
BRIEF DESCRIPTION
[0004] A distributed fuel module is provided. The distributed fuel module includes a fuel
pressure vessel with a gas port and a fuel port, a hydraulic circuit breaker connected
to the fuel port, and a gaseous circuit breaker. The gaseous circuit breaker is connected
to the gas port and is fluidly coupled with the hydraulic circuit breaker through
the fuel pressure vessel. The hydraulic circuit breaker is cooperatively associated
with the gaseous circuit breaker to isolate the fuel pressure vessel from a compressed
gas header and a fuel header according to pressure differential within the hydraulic
circuit breaker and pressure differential within the gaseous circuit breaker.
[0005] In addition to one or more of the features described above, or as an alternative,
further embodiments may include that the hydraulic circuit breaker includes a plurality
of arcuate petals supported along a flow axis, each of the arcuate petals is movable
between a flow-unobstructed open position, wherein the hydraulic circuit breaker does
not obstruct flow into the fuel port, and a flow-obstructed closed position, wherein
the hydraulic circuit breaker prevents fuel flow into the fuel port.
[0006] In addition to one or more of the features described above, or as an alternative,
further embodiments may include that the gaseous circuit breaker includes a plurality
of arcuate petals supported along a flow axis, each of the arcuate petals movable
between a flow-unobstructed open position, wherein the gaseous circuit breaker does
not obstruct flow into the gas port, and a flow-obstructed closed position, wherein
the gaseous circuit breaker prevents gas flow into the fuel pressure vessel.
[0007] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a pressure regulator connected to the fuel pressure
vessel by the gaseous circuit breaker.
[0008] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a turbine speed control valve connected to the fuel
pressure vessel by the hydraulic circuit breaker.
[0009] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a fuel header connected to the fuel pressure vessel
by the hydraulic circuit breaker.
[0010] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a compressed gas header connected to the fuel pressure
vessel by the gaseous circuit breaker.
[0011] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a liquid fuel charge contained within the fuel pressure
vessel, and a compressed gas charge contained within the compressed gas pressure vessel
and the fuel pressure vessel, the compressed gas charge urging the liquid fuel charge
toward the fuel port of the fuel pressure vessel.
[0012] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a liquid fuel flow through the hydraulic circuit breaker
in operative association with the hydraulic circuit breaker.
[0013] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a compressed gas flow through the gaseous circuit
breaker in operative association with the gaseous circuit breaker.
[0014] In addition to one or more of the features described above, or as an alternative,
further embodiments may include that the fuel pressure vessel is a first fuel pressure
vessel, that the hydraulic circuit breaker is a first hydraulic circuit breaker, and
that the gaseous circuit breaker is a first gaseous circuit breaker. The distributed
fuel module may additionally include a second fuel pressure vessel with a gas port
and a fuel port, a second hydraulic circuit breaker connected to the fuel port of
the second fuel pressure vessel, a fuel header connecting the first hydraulic circuit
breaker with the second hydraulic circuit breaker, a second gaseous circuit breaker
connected to the gas port of the second fuel pressure vessel, and a gas header connecting
the first gaseous circuit breaker with the second gaseous circuit breaker.
[0015] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a compressed gas pressure vessel with a gas port,
a gas header gaseous circuit breaker connected to the gas port of the compressed gas
pressure vessel, and a gas header connecting the gas header gaseous circuit breaker
to the gaseous circuit breaker.
[0016] In addition to one or more of the features described above, or as an alternative,
further embodiments may include that the fuel pressure vessel has no additional ports
beyond the gas port and the fuel port.
[0017] A power module is also provided. The power module includes a distributed fuel module
as described above. A liquid fuel charge is contained within the fuel pressure vessel
and a compressed gas charge is contained within the compressed gas pressure vessel
and a portion of the fuel pressure vessel, the compressed gas charge urging the liquid
fuel charge toward the fuel port of the fuel pressure vessel. A pressure regulator
is fluidly coupled to the fuel pressure vessel through the gaseous circuit breaker
by the compressed gas charge. A turbine speed control valve is fluidly coupled to
the fuel pressure vessel through the hydraulic circuit breaker by the liquid fuel
charge.
[0018] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a fuel header fluidly coupled to the fuel pressure
vessel through the hydraulic circuit breaker by the liquid fuel charge, a compressed
gas header fluidly coupled to the fuel pressure vessel through the gaseous circuit
breaker by the compressed gas charge, a liquid fuel flow through the hydraulic circuit
breaker being operatively associated with the hydraulic circuit breaker, and a compressed
gas flow through the gaseous circuit breaker is operatively associated with the gaseous
circuit breaker.
[0019] In addition to one or more of the features described above, or as an alternative,
further embodiments may include a gas generator fluidly connected to the turbine speed
control valve, a turbine fluidly connected to the gas generator, and an electric generator
operatively associated with the turbine for generator electrical power using the fuel
charge contained in the fuel pressure vessel and urged toward the turbine speed control
valve by the compressed gas charge contained in the fuel pressure vessel.
[0020] In addition to one or more of the features described above, or as an alternative,
further embodiments may include that the gas generator includes a decomposition chamber
configured to decompose a mono-propellent carried to the gas generator by the liquid
fuel charge
[0021] In addition to one or more of the features described above, or as an alternative,
further embodiments may include that the gas generator comprises a combustion chamber
configured to oxidize liquid fuel carried to the gas combustion chamber by the liquid
fuel charge.
[0022] A method of controller fuel flow in a fuel module is additionally provided. The method
includes charging a fuel pressure vessel having a gas port and a fuel port with a
liquid fuel and pressurizing the liquid fuel with a compressed gas communicated to
the fuel pressure vessel through the gas port. Liquid fuel is flowed through a hydraulic
circuit breaker connected to the fuel port when pressure differential within a hydraulic
circuit breaker is below a predetermined pressure differential. Compressed gas flows
through the gas port when the pressure differential within a gaseous circuit breaker
is below a predetermined pressure differential.
[0023] In addition to one or more of the features described above, or as an alternative,
further embodiments may include ceasing flow of liquid fuel through the hydraulic
circuit breaker when the pressure differential within the hydraulic circuit breaker
exceeds the predetermined pressure differential, and ceasing flow of compressed gas
through the gaseous circuit breaker when the pressure differential within the gaseous
circuit breaker exceeds the predetermined pressure differential.
[0024] Technical effects of the present disclosure includes the capability to retain the
capability to generate power using a pressurized distributed fuel module in the event
that one or more of the fuel pressure vessels of the distributed fuel module experiences
a breach. In certain embodiments capability is provided for two way flow to and from
depressurization-protected fuel pressure vessels, thereby allowing the fuel pressure
vessels to be charged with liquid fuel while preventing full depressurization should
one or more the depressurization-protected fuel pressure vessels be breached.
BRIEF DESCRIPTION OF THE DRAWINGS
[0025] The following descriptions should not be considered limiting in any way. With reference
to the accompanying drawings, like elements are numbered alike:
FIG. 1 is a perspective view of a power module constructed in accordance with the
present disclosure, showing a turboalternator connected to a distributed fuel module
to generate electric power using a flow of fuel provided by the distributed fuel module;
FIG. 2 is a cross-sectional view of the turboalternator of FIG. 1, showing a gas generator
fluidly connecting the distributed fuel module to a turbine of the turboalternator;
FIG. 3 is a perspective view of the distributed fuel module of FIG. 1, showing gaseous
circuit breakers and hydraulic circuit breakers connecting a compressed gas pressure
vessel to fuel pressure vessels for supplying fuel to the turboalternator;
FIG. 4 is a schematic view of the distributed fuel module of FIG. 1, showing one of
the gaseous circuit breakers and one of the hydraulic circuit breakers isolating a
breached fuel pressure vessel from the remainder of the distributed fuel module to
allow continued operation of the turboalternator notwithstanding the breach of the
fuel pressure vessel;
FIGS. 5 and 6 are cross-sectional views of a gaseous circuit breaker of the distributed
fuel module FIG. 1, showing a plurality of the petals of the gaseous circuit breaker
in flow-unobstructed, closed positions, and in flow-obstructed, open positions, respectively
according to differential pressure within the gaseous circuit breaker; and
FIG. 7 is a block diagram of a method of controlling fuel flow in a distributed fuel
module, showing steps of the method.
DETAILED DESCRIPTION
[0026] Reference will now be made to the drawings wherein like reference numerals identify
similar structural features or aspects of the subject disclosure. For purposes of
explanation and illustration, and not limitation, an exemplary embodiment of a distributed
fuel module in accordance with the disclosure is shown in FIG. 1 and is designated
generally by reference character 100. Other embodiments of distributed fuel modules,
power modules, and methods of controlling fuel flow in fuel modules in accordance
with the present disclosure, or aspects thereof, are provided in FIGS. 2-7, as will
be described. The systems and methods described herein can be used for providing fuel
from distributed fuel modules to power modules with isolation capability in the event
of breach, such as in wearable power modules in military applications, though the
present disclosure is not limited to wearable power modules or to military applications
in general.
[0027] Referring to FIG. 1, a power module 106, e.g., a wearable power module, is shown.
The power module 106 includes the distributed fuel module 100, a harness 102, and
a turboalternator 104. The harness 102 is configured and adapted for wear by a user
10 and includes a torso segment 108 and limb segment 110. The limb segment 110 includes
a left leg portion 112 and a right leg portion 114. The torso segment 108 includes
a shoulder portion 116 and a lower back portion 118. The turboalternator 104 is supported
by the lower back portion 118 of the harness 102 and the distributed fuel module 100
is supported by the limb segment 110 of the harness 102 such that the shoulder portion
116 of the torso segment 108 is free for supporting a cargo pack 12, e.g., a military-type
ruck sack. As will be appreciated by those of skill in the art in view of the present
disclosure, other types of cargo packs and mechanical loads can be supported by the
shoulder portion 116 of the torso segment 108 and remain within the scope of the present
disclosure.
[0028] With reference to FIG. 2, the turboalternator 104 is shown. The turboalternator 104
includes a gas generator 120, a turbine 122, and a connecting shaft 124. The turboalternator
104 also includes a permanent magnet generator 126 with a permanent magnet 128 and
a stator winding 130, and a power converter 132.
[0029] The gas generator 120 includes a decomposition or combustion chamber 134, is in fluid
communication with the distributed fuel module 100 (shown in FIG. 1), and is in fluid
communication with the turbine 122. The decomposition or combustion chamber 134 receives
a flow of liquid fuel 14 from the distributed fuel module 100 through a turbine speed
control valve 158, generates high pressure decomposition or combustion products 16
from the flow of liquid fuel 14, and communicates the high pressure decomposition
or combustion products 16 to the turbine 122. In certain embodiments the liquid fuel
14 is a mono-propellant like hydrazine or Otto fuel suitable for generating high pressure
decomposition products without utilization of an oxidizer. In accordance with certain
embodiments the liquid fuel can be gasoline, diesel fuel, or a kerosene-based fuel
like JP-8 suitable for generating high pressure combustion products utilizing an oxidizer,
such as compressed air.
[0030] The turbine 122 is in fluid communication with the gas generator 120 and is operatively
connected to the permanent magnet generator 126 through the connecting shaft 124.
It is contemplated that the turbine 122 be configured to receive the high pressure
decomposition or combustion products 16 from the gas generator 120, expand the high
pressure decomposition or combustion products 16, and extract work from the high pressure
decomposition or combustion products 16 to rotate the permanent magnet 128 of the
permanent magnet generator 126. In this respect the turbine 122 is operatively connected
to the permanent magnet generator 126 and communicates work extracted from the high
pressure decomposition or combustion products 16 through the connecting shaft 124
as mechanical rotation R. In certain embodiments the turbine 122 includes an impulse
turbine 136, which allows the turbine 122 to be radially compact, e.g., having a diameter
of about four (4) inches. In accordance with certain embodiments the turbine 122 includes
a single stage 138, which allows the turbine 122 to be axially compact.
[0031] The permanent magnet generator 126 is configured and adapted for generating variable
frequency alternating current (AC) power 18. In this respect the permanent magnet
128 is fixed in rotation relative to the connecting shaft 124 and is magnetically
coupled to the stator winding 130 such that rotation of the permanent magnet 128 induces
a flow of variable frequency AC current in the stator winding 130. The stator winding
130 is in turn electrically connected to the power converter 132, which converts the
variable frequency AC power 18 into direct current (DC) power 19, which the power
converter 132 communicates to an electrical load 22 connected to the power converter
132. Examples of electrical loads include directed energy weapons, exoskeletons, and
mobility and load support mechanisms.
[0032] With reference to FIG. 3, the distributed fuel module 100 is shown. The distributed
fuel module 100 includes at least one compressed gas pressure vessel 140, a first
fuel pressure vessel 142, and at least one second fuel pressure vessel 144. The distributed
fuel module 100 also includes a compressed gas header 146 with a supply gaseous circuit
breaker 148 (shown in FIG. 4), a pressure regulator 150 (shown in FIG. 4), a first
gaseous circuit breaker 152, and a second gaseous circuit breaker 154. The distributed
fuel module 100 also includes a fuel header 156 having a first hydraulic circuit breaker
157 and a second hydraulic circuit breaker 160. Although shown and described herein
in the context of an embodiment having one (1) compressed gas pressure vessel and
two (2) fuel pressure vessels, it is to be understood and appreciated that distributed
fuel modules having more than one (1) compressed gas pressure vessel and more than
two (2) fuel pressure vessels can also benefit from the present disclosure.
[0033] With reference to FIG. 4, the distributed fuel module 100 is shown schematically.
The compressed gas pressure vessel 140 has a gas port 162 and is configured for containing
within its interior a compressed gas charge 34. Examples of suitable compressed gas
charges include inert gases, such as substantially pure nitrogen, and oxidizers, such
as compressed air by way of non-limiting examples.
[0034] The first fuel pressure vessel 142 has a gas port 164, a fuel port 166, and an interior
168. It is contemplated that the first fuel pressure vessel 142 be configured to contain
within the interior 168 a liquid fuel charge 32 and a portion of the compressed gas
charge 34, which is communicated thereto by the compressed gas pressure vessel 140.
Examples of suitable liquid fuels include mono-propellants suitable for generating
high pressure flows of decomposition products in the decomposition or combustion chamber
134 (shown in FIG. 2), such as hydrazine and Otto fuel by way of non-limiting examples.
Examples of suitable liquid fuels also include liquid fuels suitable for generating
high pressure flows of combustion products in the decomposition or combustion chamber
134 utilizing an oxidizer, such as gasoline, diesel fuel, or kerosene-based fuels
like JP-8 by way of non-limiting examples. The second fuel pressure vessel 144 is
similar to the first fuel pressure vessel 142, and additionally has an interior 170,
a gas port 172, and a fuel port 173.
[0035] The compressed gas header 146 connects the compressed gas pressure vessel 140 with
the first fuel pressure vessel 142 and the second fuel pressure vessel 144. In this
respect the pressure regulator 150, the supply gaseous circuit breaker 148, the first
gaseous circuit breaker 152, and the second gaseous circuit breaker 154 are each connected
to one another by the compressed gas header 146. Specifically, the pressure regulator
150 is connected to the gas port 162 of the compressed gas pressure vessel 140. The
supply gaseous circuit breaker 148 is connected to the pressure regulator 150. The
first gaseous circuit breaker 152 is connected to the supply gaseous circuit breaker
148, is additionally connected to the gas port 164 of the first fuel pressure vessel
142, and connects the compressed gas pressure vessel 140 therethrough with the first
fuel pressure vessel 142. The second gaseous circuit breaker 154 is connected to the
supply gaseous circuit breaker 148, is additionally connected to the gas port 172
of the second fuel pressure vessel 144, and connects the compressed gas pressure vessel
140 therethrough with the second fuel pressure vessel 144.
[0036] The fuel header 156 connects the first fuel pressure vessel 142 and the second fuel
pressure vessel 144 with the turbine speed control valve 158. Specifically, the first
hydraulic circuit breaker 157 connects the fuel port 166 of the first fuel pressure
vessel 142 to the fuel header 156, and therethrough to the turbine speed control valve
158. The second hydraulic circuit breaker 160 connects the fuel port 173 of the second
fuel pressure vessel 144 to the fuel header 156, and therethrough to the turbine speed
control valve 158. This allows the compressed gas charge 34 to force fuel from the
liquid fuel charge 32 contained within the first fuel pressure vessel 142 and the
second fuel pressure vessel 144 toward the turbine speed control valve 158. The turbine
speed control valve 158 in turn regulates a flow of fuel 20 to the turboalternator
104 (shown in FIG. 1) based on a constant pressure imparted by the compressed gas
charge 34. The constant pressure is determined by the setting the pressure regulator
150, which allows the turboalternator 104 to operate without a fuel pump, such as
a variable orifice plate or other structure to throttle flow of fuel to the turboalternator
104 and thereby control the power output from the turboalternator 104.
[0037] As will be appreciated by those of skill in the art in view of the present disclosure,
breach of the compressed gas pressure vessel 140, the first fuel pressure vessel 142,
and/or the second fuel pressure vessel 144 can interfere with operation of the turboalternator
104. For example, a breach, e.g., a breach 40 in the second fuel pressure vessel 144,
can cause each of the pressure vessels within the distributed fuel module 100 to depressurize
due to the connectivity provided by the fuel header 156 and the compressed gas header
146. To limit the risk of a breach in any of the pressure vessels in the distributed
fuel module 100 causing depressurization of the remainder of the distributed fuel
module 100 gaseous circuit breakers and hydraulic circuit breakers are provided. In
this respect the supply gaseous circuit breaker 148 is connected to the gas port 162
of the compressed gas pressure vessel 140. The supply gaseous circuit breaker 148
is configured to allow fluid communication between the compressed gas pressure vessel
140 and the compressed gas header 146 when pressure differential within the supply
gaseous circuit breaker 148 is below a predetermined pressure differential, and is
further configured to isolate the compressed gas pressure vessel 140 from the compressed
gas header 146 when pressure differential within the supply gaseous circuit breaker
148 is above the predetermined value.
[0038] With reference to FIGS. 5 and 6, the supply gaseous circuit breaker 148 is shown.
The supply gaseous circuit breaker 148 includes a plurality of arcuate petals 174
arranged along a flow axis 176 and distributed circumferentially about the flow axis
176. Each of the plurality of arcuate petals 174 have a first end 178 and an axially
opposite second end 180, and are pivotably supported along the flow axis 176 at the
first end 178 such that the second end 180 is disposed radially outward of the first
end 178. Each of the plurality of arcuate petals 174 are movable between a radially
inner flow-unobstructed closed position A (shown in FIG. 5), wherein flow through
the supply gaseous circuit breaker 148 is unobstructed, and a radially outer flow-obstructed
open position B (shown in FIG. 6), wherein the flow through the supply gaseous circuit
breaker 148 is obstructed (or occluded completely). As will be appreciated by those
of skill in the art in view of the present disclosure, when in the flow-obstructed
position B, fluid communication between the compressed gas header 146 (shown in FIG.
4) and the compressed gas pressure vessel 140 is limited (or prevented entirely).
This prevents breach of the compressed gas pressure vessel 140 from depressurizing
the remainder of the distributed fuel module 100.
[0039] Movement between the flow-unobstructed closed position A and the flow-obstructed
open position B is according to a pressure differential 24 within the supply gaseous
circuit breaker 148. The pressure differential 24 is defined between a static flow
zone 28, located radially between the plurality of arcuate petals 174 and along the
flow axis 176, and a dynamic flow zone 30, located radially outward of the static
flow zone 28 and separated therefrom by the plurality of arcuate petals 174. When
the pressure differential is below a predetermined value the plurality of arcuate
petals 174 remain in the flow-unobstructed position A. When the pressure differential
exceeds the predetermined pressure differential value the plurality of arcuate petals
174 move to the flow-obstructed position B, such as when the pressure differential
24 increase due to increased flow velocity of fluid through the dynamic flow zone
30 due to a breach in the compressed gas pressure vessel 140 (shown in FIG. 4). In
certain embodiments the supply gaseous circuit breaker 148 be as shown and described
in
U.S. Patent No. 8,191,571 B2, issued on June 5, 2012.
[0040] With continuing reference to FIG. 4, it is contemplated that the first gaseous circuit
breaker 152, the first hydraulic circuit breaker 157, the second gaseous circuit breaker
154, and the second hydraulic circuit breaker 160 be similar in construction and operation
to the supply gaseous circuit breaker 148. Specifically, the second hydraulic circuit
breaker 160 is connected to the fuel port 173 of the second fuel pressure vessel 144
and the first gaseous circuit breaker 152 is connected to the gas port 164 of the
first fuel pressure vessel 142 in cooperatively association to isolate the first fuel
pressure vessel 142 from the compressed gas header 146 and the fuel header 156 according
to a pressure differential 44 within first gaseous circuit breaker 152 and a pressure
differential 46 within the first hydraulic circuit breaker 157, respectively. The
cooperation association of the first gaseous circuit breaker 152 and the first hydraulic
circuit breaker 157 causes each to close upon the acceleration of fluid flow from
either (or both) the compressed gas header 146 and the fuel header 157 in the event
of a breach developing in the first fuel pressure vessel 142. This allows the turboalternator
104 to continue operating, utilizing fuel from the second fuel pressure vessel 144
pressurized by the first compressed gas pressure vessel 140, notwithstanding a breach
of the first fuel pressure vessel 142.
[0041] Similarly, the second hydraulic circuit breaker 160 is connected to the fuel port
173 of the second fuel pressure vessel 144 and second gaseous circuit breaker 154
is connected to the gas port 172 in cooperative association to isolate the second
fuel pressure vessel 144 from the compressed gas header 146 and the fuel header 156
according to a pressure differential 52 within second gaseous circuit breaker 154
and a pressure differential 50 within the second hydraulic circuit breaker 160. The
cooperation association of the second gaseous circuit breaker 154 and the second hydraulic
circuit breaker 160 causes each to close upon the acceleration of fluid flow from
either (or both) the compressed gas header 146 and the fuel header 157 due to the
breach 40 in the second fuel pressure vessel 142. This allows the turboalternator
104 to continue operating, utilizing fuel from the first fuel pressure vessel 142
pressurized by the first compressed gas pressure vessel 140, notwithstanding the breach
40 (and depressurization) of the first fuel pressure vessel 142.
[0042] As will be appreciated, the supply gaseous circuit breaker 148 is associated with
the compressed gas header 146 to isolate the compressed gas pressure vessel 140 from
the compressed gas header 146 in the event a breach develops in the compressed gas
pressure vessel 140. In the event of such breach the turboalternator 104 would continue
to operate utilizing pressure supplied by a second compressed gas pressure vessel
connected to the compressed gas header.
[0043] With reference to FIG. 7, a method 200 of controlling fuel flow with a distributed
fuel module, e.g., the distributed fuel module 100 (shown in FIG. 1), is shown. As
shown with box 210, the method 200 includes charging a fuel pressure vessel having
a gas port and a fuel port with a liquid fuel, e.g., the first fuel pressure vessel
142 (shown in FIG. 3) and the second fuel pressure vessel 144 (shown in FIG. 3). Method
200 also includes pressurizing the liquid fuel with a compressed gas communicated
to the fuel pressure vessel through the gas port, e.g., through the gas port 164 (shown
in FIG. 3) or the gas port 172 (shown in FIG. 3), as shown with box 220.
[0044] The method 200 includes flowing liquid fuel through a hydraulic circuit breaker,
e.g., the first hydraulic circuit breaker 157 (shown in FIG. 3) or the second hydraulic
circuit breaker (shown in FIG. 3) connected to the fuel port when pressure differential
within a hydraulic circuit breaker is below a predetermined fuel flow pressure differential,
e.g., the pressure differential 44 (shown in FIG. 3) and/or the pressure differential
48 (shown in FIG. 3), as shown with box 230. Compressed gas is also communicated (i.e.,
flows) gas through the gas port when pressure differential within a gaseous circuit
breaker, e.g., the first gaseous circuit breaker 152 (shown in FIG. 3) and the second
gaseous circuit breaker 154 (shown in Fig. 3) is below a predetermined compressed
gas flow pressure differential, e.g., the pressure differential 50 (shown in FIG.
3) and the pressure differential 52 (shown in FIG. 3), as shown with box 240.
[0045] The flow of liquid fuel through the hydraulic circuit breaker ceases when the pressure
differential within the hydraulic circuit breaker exceeds the predetermined fuel flow
pressure differential, as shown with box 250. The flow of compressed gas through the
gaseous circuit breaker when the pressure differential within the gaseous circuit
breaker exceeds the predetermined compressed gas flow pressure differential, as shown
with box 260. For example, upon the second fuel pressure vessel developing a breach
40 (shown in FIG. 4), the second hydraulic circuit breaker separates the second fuel
pressure vessel from the first hydraulic pressure vessel, thereby mitigating the breach
by preventing depressurization of the remainder of the distributed fuel module 100
and allowing the power module 106 to continue to generate electrical notwithstanding
the breach.
[0046] With the advent of directed energy weapons, soldier exoskeletons, and robotic pack
mules the demand for mobile electric power has increased. Rechargeable batteries are
generally too large and heavy to support the power requirements of these devices.
Accordingly, applicant proposes to provide a wearable power module to generate electric
power using a microturbine. The microturbine is provides a flow of fuel from fuel
module including two of more fuel pressure vessels, which are distributed to accommodate
placement of cargo back on the upper shoulders of a user.
[0047] In embodiments described herein a hydraulic circuit breaker is employed to control
the flow of liquid fuel to the microturbine. In certain embodiments a compressed gas,
e.g., nitrogen, is used to pressurize a mono-propellant fuel such as hydrazine or
Otto fuel. In accordance with certain embodiments the mono-propellant or fuel is provided
to a decomposition or combustion chamber, which converts the chemical contained within
the mono-propellant or liquid fuel into thermal energy. A highly efficient single
stage impulse turbine coverts the thermal energy into mechanic energy, which is used
to drive a permanent magnet generator. While the distributed fuel module is pressurized
hydraulic circuit breakers cooperate with gaseous circuit breakers to supply the decomposition
or combustion chamber with a flow of mono-propellant or fuel while preventing, by
selectively isolating sections of the fuel module, complete depressurization of the
fuel module in the event that one of the fuel pressure vessels is breached or ruptured.
[0048] The term "about" is intended to include the degree of error associated with measurement
of the particular quantity based upon the equipment available at the time of filing
the application.
[0049] The terminology used herein is for the purpose of describing particular embodiments
only and is not intended to be limiting of the present disclosure. As used herein,
the singular forms "a", "an" and "the" are intended to include the plural forms as
well, unless the context clearly indicates otherwise. It will be further understood
that the terms "comprises" and/or "comprising," when used in this specification, specify
the presence of stated features, integers, steps, operations, elements, and/or components,
but do not preclude the presence or addition of one or more other features, integers,
steps, operations, element components, and/or groups thereof.
[0050] While the present disclosure has been described with reference to an exemplary embodiment
or embodiments, it will be understood by those skilled in the art that various changes
may be made and equivalents may be substituted for elements thereof without departing
from the scope of the invention as defined by the claims. In addition, many modifications
may be made to adapt a particular situation or material to the teachings of the present
disclosure without departing from the scope of the invention. Therefore, it is intended
that the present disclosure not be limited to the particular embodiment disclosed
as the best mode contemplated for carrying out this present disclosure, but that the
present disclosure will include all embodiments falling within the scope of the claims.
1. A distributed fuel module, comprising:
a fuel pressure vessel (142) with a gas port (164) and a fuel port (166);
a hydraulic circuit breaker (160) connected to the fuel port; and
a gaseous circuit breaker (148) connected to the gas port and fluidly coupled with
the hydraulic circuit breaker through the fuel pressure vessel,
wherein the hydraulic circuit breaker is cooperatively associated with the gaseous
circuit breaker to isolate the fuel pressure vessel from a compressed gas header and
a fuel header according to a pressure differential within the hydraulic circuit breaker
and a pressure differential within the gaseous circuit breaker.
2. The distributed fuel module as recited in claim 1, wherein the hydraulic circuit breaker
comprises a plurality of arcuate petals (174) supported along a flow axis, each of
the plurality of arcuate petals movable between a flow-unobstructed open position,
wherein the hydraulic circuit breaker does not obstruct flow into the fuel port, and
a flow-obstructed closed position, wherein the hydraulic circuit breaker prevents
fuel flow into the fuel port, and/or wherein the gaseous circuit breaker comprises
a plurality of arcuate petals (174) supported along a flow axis (176), each of the
plurality of arcuate petals movable between a flow-unobstructed open position, wherein
the gaseous circuit breaker does not obstruct flow into the gas port, and a flow-obstructed
closed position, wherein the gaseous circuit breaker prevent gas flow into the fuel
pressure vessel.
3. The distributed fuel module as recited in claim 1 or 2, further comprising a pressure
regulator (150) connected to the fuel pressure vessel by the gaseous circuit breaker
and/or further comprising a turbine speed control valve (158) connected to the fuel
pressure vessel by the hydraulic circuit breaker.
4. The distributed fuel module as recited in any preceding claim, further comprising
a fuel header (156) connected to the fuel pressure vessel by the hydraulic circuit
breaker and/or further comprising a compressed gas header (146) connected to the fuel
pressure vessel by the gaseous circuit breaker.
5. The distributed fuel module as recited in any preceding claim, further comprising:
a liquid fuel charge (32) contained within the fuel pressure vessel; and
a compressed gas charge (34) contained within the fuel pressure vessel, the compressed
gas charge urging the liquid fuel charge toward the fuel port of the fuel pressure
vessel.
6. The distributed fuel module as recited in any preceding claim, wherein a liquid fuel
flow through the hydraulic circuit breaker is operatively associated with the hydraulic
circuit breaker, and/or wherein a compressed gas flow through the gaseous circuit
breaker is operatively associated with the gaseous circuit breaker.
7. The distributed fuel module as recited in any preceding claim, wherein the fuel pressure
vessel is a first fuel pressure vessel, the hydraulic circuit breaker is a first hydraulic
circuit breaker, and the gaseous circuit breaker is a first gaseous circuit breaker,
wherein the distributed fuel module further comprises:
a second fuel pressure vessel (144) with a gas port and a fuel port (173);
a second hydraulic circuit breaker (160) connected to the fuel port of the second
fuel pressure vessel;
a fuel header (156) connecting the first hydraulic circuit breaker with the second
hydraulic circuit breaker;
a second gaseous circuit breaker (154) connected to the gas port of the second fuel
pressure vessel; and
a gas header connecting the first gaseous circuit breaker with the second gaseous
circuit breaker.
8. The distributed fuel module as recited in any preceding claim, further comprising:
a compressed gas pressure vessel (140) with a gas port;
a gaseous circuit breaker connected to the gas port of the compressed gas pressure
vessel; and
a gas header connecting the gaseous circuit breaker to the gaseous circuit breaker.
9. The distributed fuel module as recited in any preceding claim, wherein the fuel pressure
vessel has no additional ports beyond the gas port and the fuel port.
10. A power module, comprising:
a distributed fuel module as recited in any preceding claim, wherein a liquid fuel
charge is contained within the fuel pressure vessel, and wherein a compressed gas
charge is contained within the compressed gas pressure vessel and the fuel pressure
vessel, the compressed gas charge urging the liquid fuel charge toward the fuel port
of the fuel pressure vessel;
a pressure regulator fluidly coupled to the fuel pressure vessel through the gaseous
circuit breaker by the compressed gas charge; and
a turbine speed control valve fluidly coupled to the fuel pressure vessel through
the hydraulic circuit breaker by the liquid fuel charge.
11. The power module as recited in claim 10, further comprising:
a fuel header fluidly coupled to the fuel pressure vessel through the hydraulic circuit
breaker by the liquid fuel charge,
wherein a liquid fuel flow through the hydraulic circuit breaker is operatively associated
with the hydraulic circuit breaker; and
a compressed gas header fluidly coupled to the fuel pressure vessel through the gaseous
circuit breaker by the compressed gas charge, wherein a compressed gas flow through
the gaseous circuit breaker is operatively associated with the gaseous circuit breaker.
12. The power module as recited in claim 10 or 11, further comprising:
a gas generator fluidly connected to the turbine speed control valve;
a turbine fluidly connected to the gas generator; and
an electric generator operatively associated with the turbine for generator electrical
power using the fuel charge contained in the fuel pressure vessel and urged toward
the turbine speed control valve by the compressed gas charge contained in the fuel
pressure vessel.
13. The power module as recited in claim 10, 11 or 12, wherein the gas generator comprises
a decomposition chamber configured to decompose a mono-propellent carried to the gas
generator by the liquid fuel charge and/or wherein the gas generator comprises a combustion
chamber configured to oxidize liquid fuel carried to the gas combustion chamber by
the liquid fuel charge.
14. A method of controlling fuel flow in a fuel module, comprising:
charging a fuel pressure vessel having a gas port and a fuel port with a liquid fuel;
pressurizing the liquid fuel with a compressed gas communicated to the fuel pressure
vessel through the gas port;
flowing liquid fuel through a hydraulic circuit breaker connected to the fuel port
when pressure differential within a hydraulic circuit breaker is below a predetermined
fuel flow pressure differential; and
flowing compressed gas through the gas port when pressure differential within a gaseous
circuit breaker is below a predetermined compressed gas flow pressure differential.
15. The method as recited in claim 14, further comprising:
ceasing flow of liquid fuel through the hydraulic circuit breaker when the pressure
differential within the hydraulic circuit breaker exceeds the predetermined fuel flow
pressure differential; and
ceasing flow of compressed gas through the gaseous circuit breaker when the pressure
differential within the gaseous circuit breaker exceeds the predetermined compressed
gas flow pressure differential.